阳-非离子混合表面活性剂对沉积物吸附硝基苯的影响

研究了非离子表面活性剂Triton X-100、阳离子表面活性剂氯化十六烷基吡啶(CPC)及其混合物在沉积物上的吸附行为,探讨了它们对沉积物吸附硝基苯的影响.结果表明,CPC和Triton X-100在沉积物上的吸附等温线均为非线性,吸附量随着平衡浓度的增加急剧增加,并迅速达到最大吸附量.低浓度CPC能明显增加Triton X-100在沉积物上的吸附,而高浓度的CPC则显著降低Triton X-100在沉积物上的吸附.Triton X-100略微降低CPC在沉积物上的吸附.在表面活性剂浓度较低的实际环境中,无论是阳离子或非离子表面活性剂,将主要被土壤或沉积物吸附并固定.硝基苯在沉积物上的吸附等温线为线性.CPC和Triton X-100促进沉积物对硝基苯的吸附,CPC-Triton X-100混合表面活性剂溶液能进一步增强沉积物对硝基苯的吸附.因此,阳离子和非离子混合表面活性剂可增强土壤或沉积物对有机污染物的吸附固定能力,也可以用来制备有机膨润土以提高其吸附处理废水的性能.     

非离子表面活性剂溶液中多环芳烃的溶解特性

采用3种典型非离子表面活性剂(Tween80、Tween20和Triton X-100),对4种典型多环芳烃萘(naphtha-lene)、菲(phenanthrene)、芴(fluorene)和芘(pyrene)进行了溶解特性研究.结果表明,非离子表面活性剂对多环芳烃具有较好的增溶效果,在浓度大于临界胶束浓度(CMC)时,多环芳烃的溶解度与表面活性剂浓度成正比例线性相关通过质量溶解率(WSR)的比较,确定3种非离子表面活性剂对多环芳烃的增溶效果为Triton X-100＞Tween80＞Tween20,与其HLB值呈负相关.在非离子表面活性剂溶液中,多环芳烃的正辛醇-水分配系数(K_ow)与其胶束-水分配系数(K_m)呈现良好的线性相关关系.     

表面活性剂对极性有机物在沉积物上吸附的影响

研究了苯酚、苯胺和对硝基苯酚在沉积物-十二烷基苯磺酸钠(SDBS)体系中的分配特性.结果表明200mg/L和1200mg/L的SDBS存在下,苯胺和对硝基苯酚的沉积物-水分配系数均增大,分配作用的增大倍数与有机物的K_ow呈正相关;苯酚的分配系数则因表面活性剂存在浓度的不同分别增大和减小.十二烷基硫酸钠(SDS)、Triton X-100(TX100)和Brij30存在下,苯酚等温吸附实验表明:表面活性剂浓度约低于其临界胶束浓度(CMC)时,苯酚的吸附量增大;表面活性剂浓度约高于其CMC时,苯酚的吸附量比纯水中的吸附量小.     

非一阴离子表面活性剂对PAHs的增溶作用及无机盐的强化效果研究

文章研究了几种非离子和阴离子表面活性剂在单一或混合条件下对多环芳烃（PAHs）萘和菲的增溶作用,并分析了无机盐对表面活性剂增溶PAHs的强化效果.结果表明,在相同浓度条件下,非离子表面活性剂对菲和萘的增溶效果均高于阴离子表面活性剂,其增溶能力大小顺序为：Tween 80 ＞TX-100＞ Tween 20＞ SDS＞SDBS.将非离子与阴离子表面活性剂混合后,对萘和菲的增溶作用大于单一阴离子表面活性剂而小于单一非离子表面活性剂,且增溶效果随着非离子表面活性剂比例的增加而增大.低浓度（0.03 mol/L）的NaCl和Na2SO4可大幅度促进表面活性剂对萘和菲的增溶效果,但随着无机盐浓度的提高,对增溶效果的促进作用不明显.     

非-阴离子表面活性剂对PAHs的增溶作用及无机盐的强化效果研究

文章研究了几种非离子和阴离子表面活性剂在单一或混合条件下对多环芳烃(PAHs)萘和菲的增溶作用,并分析了无机盐对表面活性剂増溶PAHs的强化效果。结果表明,在相同浓度条件下,非离子表面活性剂对菲和萘的增溶效果均高于阴离子表面活性剂,其增溶能力大小顺序为:Tween 80TX-100Tween 20SDSSDBS。将非离子与阴离子表面活性剂混合后,对萘和菲的增溶作用大于单一阴离子表面活性剂而小于单一非离子表面活性剂,且增溶效果随着非离子表面活性剂比例的增加而增大。低浓度(0.03 mol/L)的NaCl和Na2SO4可大幅度促进表面活性剂对萘和菲的增溶效果,但随着无机盐浓度的提高,对增溶效果的促进作用不明显。     

芘污染黑土的表面活性剂洗脱修复研究

采用批量平衡振荡法研究了几种阴离子和非离子表面活性剂对黑土中芘的洗脱效果,以及不同因素对洗脱效果的影响。结果表明,非离子表面活性剂对芘的洗脱效果优于阴离子表面活性剂。将SDS和Triton X-100以不同质量配比混合后,可提高其洗脱效果,尤其在质量配比为3∶7时洗脱效果最好。不同固液比条件可影响Triton X-100对芘的洗脱,Triton X-100在低浓度时,固液比为1∶30时的洗脱效果最好;浓度大于5.0 g/L后,固液比为1∶10时的洗脱效果最好。Triton X-100对土壤中低浓度芘的洗脱效果要好于土壤中高浓度的芘。萘在土壤中的共存会降低Triton X-100对芘的洗脱率,萘浓度越高,芘的洗脱率越低。Triton X-100对不同类型土壤中芘的洗脱效果相差不大,对新疆荒漠土的洗脱效果好于哈尔滨黑土,这可能与土壤有机质含量有关。     

表面活性剂去除土壤和地下水中LNAPLs作用机制研究

去除多孔介质中滞留的LNAPLs,表面活性剂对LNAPLs的增溶和降低界面张力是关键.在实验测得不同浓度Triton X-100溶液对正十六烷的增溶以及它们之间界面张力的基础上,通过平衡清洗实验和砂柱冲洗实验分析了不同形态正十六烷的产生规律和机制.结果表明,正十六烷溶解能力与Triton X-100浓度成正比,当Triton X-100浓度大于临界胶束浓度CMC时,计算得摩尔增溶比MSR=1.680 4,胶束相/水相分配系数对数值lgK_mc=1.715 8;正十六烷-Triton X-100溶液之间界面张力与Triton X-100浓度成反比,其变化规律符合高斯模型（R₂=0.996 4）;溶解态正十六烷和自由态正十六烷与增溶和降低界面张力分别有较好的对应关系,表明增溶和降低界面张力都对多孔介质中正十六烷去除有影响,其中降低界面张力可以有效增加多孔介质中正十六烷的流动性,在正十六烷去除过程中起主要作用.     

共存有机物对毒死蜱在沉积物上吸附的影响

用批量平衡法研究了共存有机物对毒死蜱在沉积物上吸附行为的影响.结果表明,苯酚和芘对毒死蜱在沉积物上的吸附有竞争作用,其中苯酚的竞争能力较大.多种有机污染物共存时,毒死蜱在沉积物上的吸附仍然由分配作用决定.表面活性剂的浓度小于临界胶束浓度(CMC)时,十二烷基硫酸钠(SDS)能明显降低毒死蜱在沉积物上的吸附量,降低程度与SDS浓度呈负相关,而非离子表面活性剂Triton X-100能增加毒死蜱在沉积物上的吸附量,增加程度与Triton X-100浓度呈正相关.     

醇类助溶剂去除砂土中多氯联苯作用机制

醇类助溶剂单一使用及复配表面活性剂使用去除砂土中多氯联苯(PCBs)的关键是增溶和降低界面张力.通过降低界面张力实验和振荡增溶实验分析了醇类助溶剂单一使用对多氯联苯界面张力的降低作用和增溶作用,以及醇类复配Triton X-100使用时醇对Triton X-100降低界面张力和增溶PCBs的影响.结果表明,醇-PCBs油的界面张力与醇浓度、醇含碳原子数均呈负相关,甲醇、乙醇、异丙醇的最佳解吸浓度分别为70%、55%、40%,最佳解吸效率达90%以上;Triton X-100-PCBs油界面张力与Triton X-100浓度呈负相关,Triton X-100浓度低于3 000 mg/L时复配10%乙醇、10%异丙醇比单一Triton X-100振荡洗脱效率低,Triton X-100浓度在3 000～7 500 mg/L时3组差异不大,Triton X-100浓度为10 000 mg/L时单一、10%乙醇、10%异丙醇TritonX-100溶液解吸效率分别为80.9%、90.36%、89.36%.表明醇类单一使用对降低界面张力与增溶均有很好的效果,但需要其体积分数达40%以上;醇类复配Triton X-100时醇的存在弱化了Triton X-100增溶和降低界面张力的作用,乙醇与异丙醇弱化作用差异性不大,当Triton X-100浓度高于3 000 mg/L时,弱化作用不显著.     

几种表面活性剂洗脱修复苊污染黑土研究

采用批量平衡振荡法研究了几种阴离子和非离子表面活性剂在单一使用和混合使用条件下对苊污染黑土的洗脱作用及影响因素。结果表明:4种表面活性剂对苊洗脱率的大小顺序为SDBS>SDS>Triton X-100>Tween40,且浓度越大,洗脱效果越好。将SDBS和Triton X-100按一定质量比例混合后可大幅度提高苊的洗脱率,不同质量比的苊洗脱率大小顺序为1∶9>1∶3>9∶1>1∶1>3∶1。水土比为20∶1的条件下,SDBS对苊污染黑土洗脱能力最高,15∶1时次之,10∶1时最低。NaCl和MgCl_2在低浓度条件下即可大幅度降低SDBS对黑土中苊的洗脱率。菲-苊混合污染土壤中,菲的存在使表面活性剂对苊的洗脱率下降。     

五种表面活性剂对柴油污染土壤清洗效果的比较

研究了十二烷基硫酸钠(SDS)、十二烷基苯磺酸钠(SDBS)、皂苷(saponin)、月桂醇聚氧乙烯(23)醚(Brij35)、Triton X-100五种表面活性剂对中度柴油污染土壤的清洗效果,考察柴油和土壤混合后在不同时间段的挥发特点,认为污染时长会直接影响表面活性剂清洗修复的效果,增大清洗剂浓度可以提高对新污染土壤的洗脱率,但对老化污染土壤的效果并不明显;对不同含油量的污染土壤清洗,研究污染程度对洗脱率变化的影响,当达到一定含油量后洗脱效果产生突变。不同表面活性剂在相同CMC倍数下清洗能力存在差异,其顺序为SDS>SDBS>Triton X-100>皂苷>Brij35。     

Mobilization of arsenic from contaminated sediment by anionic and nonionic surfactants

The increasing manufacture of surfactants and their wide application in industry,agriculture and household detergents have resulted in large amounts of surfactant residuals being discharged into water and distributed into sediment. Surfactants have the potential to enhance arsenic mobility, leading to risks to the environment and even human beings. In this study, batch and column experiments were conducted to investigate arsenic mobilization from contaminated sediment by the commercial anionic surfactants sodium dodecylbenzenesulfonate(SDBS), sodium dodecyl sulfate(SDS), sodium laureth sulfate(AES)and nonionic surfactants phenyl-polyethylene glycol(Triton X-100) and polyethylene glycol sorbitan monooleate(Tween-80). The ability of surfactants to mobilize arsenic followed the order AES SDBS SDS ≈ Triton X-100 Tween 80. Arsenic mobilization by AES and Triton X-100 increased greatly with the increase of surfactant concentration and p H, while arsenic release by SDBS, SDS and Tween-80 slightly increased. The divalent ion Ca~(2+) caused greater reduction of arsenic mobilization than Na~+. Sequential extraction experiments showed that the main fraction of arsenic mobilized was the specifically adsorbed fraction. Solid phase extraction showed that arsenate(As(V)) was the main species mobilized by surfactants,accounting for 65.05%–77.68% of the total mobilized arsenic. The mobilization of arsenic was positively correlated with the mobilization of iron species. The main fraction of mobilized arsenic was the dissolved fraction, accounting for 70% of total mobilized arsenic.     

Adsorption of mixed cationic-nonionic surfactant and its effect on bentonite structure

The adsorption of cationic-nonionic mixed surfactant onto bentonite and its effect on bentonite structure were investigated. The objective was to improve the understanding of surfactant behavior on clay mineral for its possible use in remediation technologies of soil and groundwater contaminated by toxic organic compounds. The cationic surfactant used was hexadecylpyridinium bromide (HDPB), and the nonionic surfactant was Triton X-100 (TX100). Adsorption of TX100 was enhanced significantly by the addition of HDPB, but this enhancement decreased with an increase in the fraction of the cationic surfactant. Part of HDPB was replaced by TX100 which decreased the adsorption of HDPB. However, the total adsorbed amount of the mixed surfactant was still increased substantially, indicating the synergistic effect between the cationic and nonionic surfactants. The surfactant-modified bentonite was characterized by Brunauer-Emmett-Teller specific surface area measurement, Fourier transform infrared spectroscopy, and thermogravimetric-derivative thermogravimetric/differential thermal analyses. Surfactant intercalation was found to decrease the bentonite specific surface area, pore volume, and surface roughness and irregularities, as calculated by nitrogen adsorption-desorption isotherms. The co-adsorption of the cationic and nonionic surfactants increased the ordering conformation of the adsorbed surfactants on bentonite, but decreased the thermal stability of the organobentonite system.     

Sorption and transport studies of cetyl trimethylammonium bromide (CTAB) and Triton X-100 in clayey soil

Surfactants are soil washing agents and facilitators for subsurface remediation of hydrocarbon spills.It is important to understand the sorption and transport behavior of surfactants for enhanced soil remediation.The adsorption and desorption isotherms of cetyl trimethylammonium bromide (CTAB) and Triton X-100 with sand and kaolinite have been quantified.Kaolinite clay had the highest sorption capacity compared to blasting sand.Transport parameters such as diffusion coefficient (D) and retardation factor (R) of the above mentioned surfactant solutions were determined in clayey soils (82.5% sand and 17.5% kaolinite mixture) with near zero and 0.1 g/L ionic strength.NaCl was used as the electrolyte solution.Convection-Diffusion equation was used to model the breakthrough curves of the surfactants.Bromide ion was chosen as the tracer material in order to characterize the column.CTAB and Triton X-100 were used to flush the perchloroethylene (PCE) contaminated soil.The effectiveness of CTAB and Triton X-100 in flushing the PCE from the contaminated soil was quantified.     

Solubilization and degradation of perchloroethylene （PCE） in cationic and nonionic surfactant solutions

Solubilization of perchloroethylene (PCE) in a nonionic (Triton X-100) and a cationic (cetyltrimethylammonium bromide (CTAB)) surfactant solutions and the degradation of surfactant solubilized PCE using fine to nanosize Fe and bi-metallic Fe-Ni particles were investigated. Micelle partition coefficients (Km) and molar solubility ratio (MSR) for PCE in 10 g/L of surfactant solutions have been quantified and the solubility of PCE (100 mg/L in water) in the surfactant solutions increased by about ten fold. Of the two surfactants studied, Triton X-100 solubilized the higher amount of PCE per gram of surfactant. To degrade solubilized PCE, both iron and bimetallic Fe-Ni particles were used in continuously stirred batch reactors. The iron and bi-metallic particles were synthesized using the solution method and the particles were characterized using the SEM, EDS, TEM and XRD. The PCE solubilized up to 500 mg/L in both surfactant solutions were totally degraded at various rates by 200 g/L of bi-metallic Fe-Ni particles in less than 20 hr, which is the highest concentration of PCE degraded in the shortest time compared to data in the literature. The degradations of PCE solubilized in surfactant solutions were represented by nonlinear kinetic relationships which depended on the type of surfactant used for solubilizing the PCE.     

Sorption of Triton X-100 on soil organic matter fractions：Kinetics and isotherms

Kinetics and isotherms of Triton X-100 sorption on soil,base-extracted soil(BE),humic acid (HA) and humin (HM) were investigated respectively to get better understanding on characteristics of the surfactant sorptiun onto different soil organic matters(SOMs).It was demonstrated that the kinetics results could be satisfactorily described by the pseudo-second order model.The half of the time to reach equilibrium(t1/2) for different sorbents followed the sequence of soil>HA>BE>HM.Furthermore,the calculated equilibrium sorption capacity(Ceq) was found in the sequence of HA>BE>HM>soil,which agreed well with the experimental results.The isotherms of Triton X-100 sorption on soil and HA could be well described by the S-type isotherm,but BE and HM by the L-type.The isotherms of all the four sorbents were found reasonably fitted to the Langmuir equation.The Kd value,defined as the ratio of Triton X-100 in sorbent and in the equilibrium solution for given concentrations,generally followed the order of HM>HA>soil>BE.Separated HM and HA showed high affinity for Triton X-100,but the HA and HM in soil and BE were tightly bounded by the minerals.Thus,the HA on the soil surface might dominate the sorption,whereas the bounded HM would play a key role upon the surfactants being penetrated inside the soil.     

Arsenic retention and transport behavior in the presence of typical anionic and nonionic surfactants

The massive production and wide use of surfactants have resulted in a large amount of surfactant residuals being discharged into the environment,which could have an impact on arsenic behavior.In the present study,the influence of the anionic surfactant sodium dodecyl benzene sulfonate(SDBS) and nonionic surfactant polyethylene glycol octylphenyl ether(Triton X-100) on arsenic behavior was investigated in batch and column tests.The presence of SDBS and Triton X-100 reduced arsenic retention onto ferrihydrite(FH),enhanced arsenic transport through FH coated sand(FH-sand) columns and promoted arsenic release from the FH surface.With coexisting surfactants in solution,the equilibrium adsorbed amount of arsenic on FH decreased by up to 29.7% and the adsorption rate decreased by up to 52.3%.Pre-coating with surfactants caused a decrease in the adsorbed amount and adsorption rate of arsenic by up to 15.1% and 58.3%,respectively.Because of the adsorption attenuation caused by surfactants,breakthrough of As(Ⅴ) and As(Ⅲ) with SDBS in columns packed with FH-sand was 23.8% and 14.3%faster than that in those without SDBS,respectively.In columns packed with SDBS-coated FH-sand,transport of arsenic was enhanced to a greater extent.Breakthrough of As(Ⅴ) and As(Ⅲ) was 52.4% and 43.8% faster and the cumulative retention amount was 44.5% and 57.3% less than that in pure FH-sand column systems,respectively.Mobilization of arsenic by surfactants increased with the increase of the initial adsorbed amount of arsenic.The cumulative release amount of As(Ⅴ) and As(Ⅲ) from the packed column reached 10.8% and 36.0%,respectively.     

Effects of surfactants on graphene oxide nanoparticles transport in saturated porous media

Transport behaviors of graphene oxide nanoparticles (GONPs) in saturated porous media were examined as a function of the presence and concentration of anionic surfactant (SDBS) and non-ionic surfactant (Triton X-100) under different ionic strength (IS). The results showed that the GONPs were retained obviously in the sand columns at both IS of 50 and 200 mmol/L, and they were more mobile at lower IS. The presence and concentration of surfactants could enhance the GONP transport, particularly as observed at higher IS. It was interesting to see that the GONP transport was surfactant type dependent, and SDBS was more effective to facilitate GONP transport than Triton X-100 in our experimental conditions. The advection–dispersion–retention numerical modeling followed this trend and depicted the difference quantitatively. Derjaguin–Landau–Verwey–Overbeek (DLVO) interaction calculations also were performed to interpret these effects, indicating that secondary minimum deposition was critical in this study.     

Effects of nonionic surfactant Triton X-100 on the laccase-catalyzed conversion of bisphenol A

The laccase-catalyzed conversion of bisphenol A (BPA) in aqueous solutions was studied in the absence and presence of nonionic surfactant Triton X-100. It was found that the addition of Triton X-100 into the reaction system increased the conversion of BPA, especially near the critical micelle concentration of Triton X-100. Also it was found that the stability of laccase was greatly improved in the presence of TritonX-100. Studies on the endogenous fluorescence emission of laccase indicated that there existed an interaction between Triton X-100 and laccase, which was beneficial to folding and stabilizating of laccase. The binding of Triton X-100 to the laccase surface also mitigated the inactivation e ect caused by the free radicals and polymerization products. Under otherwise identical conditions, a lower dosage of laccase was needed for the higher conversion of BPA in the presence of Triton X-100.